CN101265073B - Composite silica brick and its preparation method - Google Patents
Composite silica brick and its preparation method Download PDFInfo
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- CN101265073B CN101265073B CN2008100495672A CN200810049567A CN101265073B CN 101265073 B CN101265073 B CN 101265073B CN 2008100495672 A CN2008100495672 A CN 2008100495672A CN 200810049567 A CN200810049567 A CN 200810049567A CN 101265073 B CN101265073 B CN 101265073B
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 211
- 239000000377 silicon dioxide Substances 0.000 title claims abstract description 87
- 239000011449 brick Substances 0.000 title claims abstract description 75
- 239000002131 composite material Substances 0.000 title claims abstract description 17
- 238000002360 preparation method Methods 0.000 title claims abstract description 6
- 239000000843 powder Substances 0.000 claims abstract description 50
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 47
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims abstract description 28
- 239000002245 particle Substances 0.000 claims abstract description 25
- 229910000019 calcium carbonate Inorganic materials 0.000 claims abstract description 22
- 239000005543 nano-size silicon particle Substances 0.000 claims abstract description 16
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 15
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 15
- 239000004571 lime Substances 0.000 claims abstract description 15
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims abstract description 13
- 239000010436 fluorite Substances 0.000 claims abstract description 13
- 239000011858 nanopowder Substances 0.000 claims abstract description 11
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims description 11
- 229910052710 silicon Inorganic materials 0.000 claims description 11
- 239000010703 silicon Substances 0.000 claims description 11
- 239000000292 calcium oxide Substances 0.000 claims description 9
- 239000000920 calcium hydroxide Substances 0.000 claims description 7
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 238000005245 sintering Methods 0.000 claims description 6
- 239000002002 slurry Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 4
- 239000008267 milk Substances 0.000 claims description 4
- 210000004080 milk Anatomy 0.000 claims description 4
- 235000013336 milk Nutrition 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 238000009736 wetting Methods 0.000 claims description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims 10
- 239000002105 nanoparticle Substances 0.000 claims 4
- 238000002156 mixing Methods 0.000 claims 3
- 229910004298 SiO 2 Inorganic materials 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 239000004615 ingredient Substances 0.000 claims 1
- 239000011236 particulate material Substances 0.000 claims 1
- 238000003825 pressing Methods 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 23
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 18
- 238000004519 manufacturing process Methods 0.000 abstract description 13
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 abstract description 12
- 239000007788 liquid Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 10
- 239000010453 quartz Substances 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 9
- 230000009466 transformation Effects 0.000 abstract description 7
- 239000006185 dispersion Substances 0.000 abstract description 5
- 239000011230 binding agent Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 239000002114 nanocomposite Substances 0.000 abstract description 4
- 238000009826 distribution Methods 0.000 abstract description 3
- 239000011148 porous material Substances 0.000 abstract description 3
- 230000007423 decrease Effects 0.000 abstract 2
- 238000002425 crystallisation Methods 0.000 abstract 1
- 230000008025 crystallization Effects 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 238000010304 firing Methods 0.000 description 13
- 239000007791 liquid phase Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 10
- 229910052906 cristobalite Inorganic materials 0.000 description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 7
- 229910052905 tridymite Inorganic materials 0.000 description 6
- 229910052681 coesite Inorganic materials 0.000 description 4
- 229910052682 stishovite Inorganic materials 0.000 description 4
- 229910021489 α-quartz Inorganic materials 0.000 description 4
- 230000033558 biomineral tissue development Effects 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 239000011268 mixed slurry Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 238000009628 steelmaking Methods 0.000 description 2
- OBNDGIHQAIXEAO-UHFFFAOYSA-N [O].[Si] Chemical compound [O].[Si] OBNDGIHQAIXEAO-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000011820 acidic refractory Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical group [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- UHZZMRAGKVHANO-UHFFFAOYSA-M chlormequat chloride Chemical compound [Cl-].C[N+](C)(C)CCCl UHZZMRAGKVHANO-UHFFFAOYSA-M 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000011044 quartzite Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Compositions Of Oxide Ceramics (AREA)
Abstract
一种纳米复合硅砖及其制备方法,其特征是:硅砖原料及结合剂包括:硅石颗粒和细粉、废硅砖颗粒、纳米碳酸钙、纳米氧化铁、纳米二氧化硅、萤石粉、石灰、亚硫酸纸浆废液。本发明以目前硅砖的常规生产工艺为基础,将复合纳米粉体以最佳比例配合、经高效分散后引入硅砖的制砖工艺中,制得纳米复合的硅砖。加入纳米粉后硅砖的性能显著提高,具体体现在:1)使粒度级配更合理,堆积紧密,结构均匀;2)泥料可塑性强,成型性能好,生产效率提高;3)可降低烧成温度20℃,节能降耗效果明显;4)磷石英结晶转化好,残余石英含量低;5)闭口气孔增加,开口气孔减少,气孔率下降,强度和荷重软化温度提高;6)产品外观好,端口表面光滑,结合良好,成品合格率提高。A nanocomposite silica brick and its preparation method, characterized in that: the silica brick raw material and binder include: silica particles and fine powder, waste silica brick particles, nano calcium carbonate, nano iron oxide, nano silicon dioxide, fluorite powder, Lime, sulfurous acid pulp waste liquid. The present invention is based on the conventional production process of silica bricks at present, mixes composite nanometer powder in an optimal ratio, introduces it into the brick making process of silica bricks after efficient dispersion, and prepares nanocomposite silica bricks. The performance of silica bricks is significantly improved after adding nano powder, which is embodied in: 1) the particle size distribution is more reasonable, the packing is tight, and the structure is uniform; 2) the mud has strong plasticity, good forming performance, and improved production efficiency; 3) it can reduce burning. The forming temperature is 20°C, and the effect of energy saving and consumption reduction is obvious; 4) Phospho-quartz crystallization transformation is good, and the residual quartz content is low; 5) The closed pores increase, the open pores decrease, the porosity decreases, and the strength and load softening temperature increase; 6) The appearance of the product is good , The surface of the port is smooth, the combination is good, and the qualified rate of the finished product is improved.
Description
技术领域technical field
本发明属于无机非金属材料技术领域(耐火材料),具体涉及一种复合硅砖及其制备方法,使用的多种纳米粉指的是纳米碳酸钙、纳米氧化铁和纳米二氧化硅。The invention belongs to the technical field of inorganic non-metallic materials (refractory materials), and specifically relates to a composite silica brick and a preparation method thereof. The various nano powders used refer to nano calcium carbonate, nano iron oxide and nano silicon dioxide.
背景技术Background technique
硅砖是一种以SiO2为主要成分的传统耐火制品,属酸性耐火材料,具有高温体积稳定性和导热性好、抗酸性渣侵蚀性优良、特别是荷重软化温度高(与耐火度仅有30~50℃之差)等特点。制造硅砖的主要原料是硅石(石英岩),我国从20世纪30年代开始生产一般硅砖,至50年代初开始大量生产炼钢平炉和焦炉用硅砖。半个世纪以来,随着炼钢平炉的淘汰,硅砖的使用目前主要集中在焦炉、高炉及玻璃窑,然而,在相当长的时期内硅砖的制造工艺和技术未发生大的变化。Silica brick is a traditional refractory product with SiO2 as the main component. It is an acidic refractory material. It has high temperature volume stability, good thermal conductivity, excellent resistance to acid slag erosion, and especially a high softening temperature under load (only the same as the refractoriness. 30 ~ 50 ℃ difference) and other characteristics. The main raw material for making silica bricks is silica (quartzite). Our country began to produce general silica bricks in the 1930s, and began to mass produce silica bricks for steelmaking open hearth furnaces and coke ovens in the early 1950s. For half a century, with the elimination of steelmaking open hearth furnaces, the use of silica bricks is currently mainly concentrated in coke ovens, blast furnaces and glass kilns. However, the manufacturing process and technology of silica bricks have not undergone major changes for a long period of time.
由于硅石在加热过程中的快速晶型转变产生较大体积膨胀,使硅砖的烧成比其它耐火材料困难。制造硅砖的核心技术是矿化剂的选择与应用,其目的是为了控制硅砖在烧成过程中、由于硅石的晶型转变在砖内产生较大应力引起的体积膨胀,避免硅砖在烧成时开裂。硅砖烧成时要求将石英尽可能的转变为稳定的高温矿物相鳞石英和方石英,为了促进这种转化,通常在制作硅砖过程中加入矿化剂。矿化剂是可与SiO2反应生成液相的氧化物,其作用是在加速石英转化的同时不显著降低制品的耐火度,并能抑制砖坯烧成时因膨胀产生的应力,防止制品疏松或开裂。Due to the large volume expansion caused by the rapid crystal transformation of silica during heating, the firing of silica bricks is more difficult than other refractory materials. The core technology of making silica bricks is the selection and application of mineralizers, the purpose of which is to control the volume expansion of silica bricks caused by the large stress in the bricks due to the crystal transformation of silica during the firing process, so as to prevent the silica bricks from Cracks when fired. When firing silica bricks, it is required to convert quartz into stable high-temperature mineral phases tridymite and cristobalite as much as possible. In order to promote this transformation, mineralizers are usually added in the process of making silica bricks. Mineralizer is an oxide that can react with SiO2 to form a liquid phase. Its function is to accelerate the transformation of quartz without significantly reducing the refractoriness of the product, and can inhibit the stress caused by expansion when the brick is fired, preventing the product from loosening or cracking.
制造工艺决定硅砖的矿相组成和产品质量,在同一烧成温度下,矿化剂的品种、粒度和加入量决定了矿相的组成和相对含量。当矿化剂存在时,石英的转化过程是:1β-石英在573℃快速转化为α-石英,在1200~1470℃范围内,α-石英快速转化为亚稳定方石英。同时α-石英、亚稳方石英和矿化剂及杂质等相互作用形成液相,并侵入石英颗粒以及形成亚稳方石英时产生的裂纹中,促进α-石英和亚稳方石英不断地溶解于所形成的液相中,使之成为硅氧的过饱和熔体,然后以稳定的鳞石英形态逐渐从熔体中结晶出来,该过程的转化速度取决于矿化剂的理化性质和数量。矿化剂作用能力的大小,主要取决于矿化剂与砖坯中硅氧在高温时所形成熔体的性质及其分布状态和数量,即:液相开始形成的温度,液相的粘度和润湿能力,液相的结构、数量、分布等因素。The manufacturing process determines the mineral phase composition and product quality of silica bricks. At the same firing temperature, the type, particle size and amount of mineralizer determine the mineral phase composition and relative content. When the mineralizer exists, the transformation process of quartz is: 1β-quartz rapidly transforms into α-quartz at 573°C, and in the range of 1200-1470°C, α-quartz rapidly transforms into metastable cristobalite. At the same time, α-quartz, metastable cristobalite interacts with mineralizers and impurities to form a liquid phase, and invades quartz particles and cracks generated when metastable cristobalite is formed, promoting the continuous dissolution of α-quartz and metastable cristobalite In the formed liquid phase, it becomes a supersaturated melt of silicon and oxygen, and then gradually crystallizes out of the melt in the form of stable tridymite. The conversion speed of this process depends on the physical and chemical properties and quantity of the mineralizer. The action capacity of the mineralizer mainly depends on the properties of the melt formed by the mineralizer and silicon oxygen in the brick adobe at high temperature, as well as its distribution and quantity, namely: the temperature at which the liquid phase begins to form, the viscosity and the wetness of the liquid phase. Wetting capacity, liquid phase structure, quantity, distribution and other factors.
理想的矿化剂应具备如下条件:An ideal mineralizer should meet the following conditions:
1)应能够与SiO2作用,在相对较低的温度下形成液相(一般在1300℃以下),且对制品的耐火度影响不大;1) It should be able to interact with SiO2 to form a liquid phase at a relatively low temperature (generally below 1300°C), and have little effect on the refractoriness of the product;
2)生成液相的粘度较低,对石英颗粒表面有较好的润湿性;2) The viscosity of the generated liquid phase is low and has good wettability to the surface of quartz particles;
3)生成的液相量随温度的升高变化不大;3) The amount of liquid phase generated does not change much with the increase of temperature;
4)在制砖过程中矿化剂应尽可能地分散且分布均匀;4) The mineralizer should be dispersed and evenly distributed as much as possible during the brick making process;
5)矿化剂不具有水溶性,在砖坯干燥时不迁移析出。5) The mineralizer is not water-soluble, and does not migrate and precipitate when the brick is dried.
目前制作硅砖实际使用的矿化剂大多是氧化铁和氧化钙,它们不仅具有上述特点,且能保证硅砖具有很好的高温力学性能。但是,生产中使用的氧化铁和氧化钙分别以细粉形式和石灰乳形式加入,相对纳米级的粉体而言,前者粒度不够细,在硅砖中分散不够均匀;后者实际上加入的是氢氧化钙,其石灰乳溶液容易絮凝,不易分散,因此作为矿化剂的效果较差。而采用纳米级的矿化剂不仅使得其分散均匀程度大大提高,同时可以改善硅砖的显微结构,促进烧结,降低烧成温度,提高制品的性能。At present, most of the mineralizers used in the production of silica bricks are iron oxide and calcium oxide. They not only have the above characteristics, but also can ensure that silica bricks have good high-temperature mechanical properties. However, iron oxide and calcium oxide used in production are added in the form of fine powder and milk of lime respectively. Compared with nano-scale powder, the particle size of the former is not fine enough, and the dispersion in the silica brick is not uniform enough; the latter actually adds It is calcium hydroxide, and its lime milk solution is easy to flocculate and not easy to disperse, so the effect as a mineralizer is poor. The use of nano-scale mineralizers not only greatly improves the uniformity of dispersion, but also improves the microstructure of silica bricks, promotes sintering, reduces the firing temperature, and improves the performance of products.
发明内容Contents of the invention
本发明的目的是针对上述硅砖生产现有技术中所存在的问题而研制的一种复合硅砖(纳米碳酸钙、纳米氧化铁、纳米二氧化硅)及其制备方法。The object of the present invention is to develop a kind of composite silica brick (nano-calcium carbonate, nano-iron oxide, nano-silicon dioxide) and preparation method thereof for the problems existing in the prior art of above-mentioned silica brick production.
本发明目的在于利用纳米二氧化硅粉体的填充作用以提高制品的体积密度;利用纳米碳酸钙粉体粒度细小、容易分解、分解后生成高活性的氧化钙以及纳米氧化铁的高分散、高效矿化等优点,来改善目前硅砖生产中所用矿化剂的缺点,制备出一种性能优异的纳米复合硅砖。The purpose of the present invention is to use the filling effect of nano-silica powder to increase the bulk density of the product; to use the nano-calcium carbonate powder with fine particle size, easy to decompose, and generate highly active calcium oxide after decomposition, and the high dispersion and high efficiency of nano-iron oxide Mineralization and other advantages to improve the shortcomings of the mineralizers currently used in the production of silica bricks, and prepare a nanocomposite silica brick with excellent performance.
本发明是通过以下技术方案来实现的:本发明含有多种纳米粉的硅砖使用的原料和结合剂包括:硅石颗粒和细粉、废硅砖颗粒、纳米碳酸钙、纳米氧化铁、纳米二氧化硅、萤石粉、石灰、亚硫酸纸浆废液,各原料的重量百分比范围如下:The present invention is achieved through the following technical solutions: the raw materials and binders used in the silica brick containing various nanopowders in the present invention include: silica particles and fine powder, waste silica brick particles, nano calcium carbonate, nano iron oxide, nano Silica, fluorite powder, lime, sulfurous acid pulp waste liquid, the weight percent scope of each raw material is as follows:
硅石颗粒和细粉 80~90%Silica granules and fine powder 80-90%
废硅砖颗粒 5~15%Waste silica brick particles 5~15%
纳米碳酸钙 0.5~2%Nano calcium carbonate 0.5~2%
纳米氧化铁 0.5~2%Nano iron oxide 0.5~2%
纳米二氧化硅 1.0~2%Nano silica 1.0~2%
石灰 0.5~2%Lime 0.5~2%
萤石粉 0.2~1%Fluorite powder 0.2~1%
亚硫酸纸浆废液 0.5~2%Sulfurous acid pulp waste liquid 0.5~2%
在本发明的整个原料中,骨料(即硅石和废硅砖颗粒)与细粉的质量比例为(60%~70%)/(40%~30%),硅石的化学成分要求为SiO2≥98.0%。In the whole raw material of the present invention, the mass ratio of aggregate (i.e. silica and waste silica brick particles) to fine powder is (60%-70%)/(40%-30%), and the chemical composition of silica is required to be SiO2 ≥98.0%.
所使用的纳米碳酸钙是指粒度小于100nm的亲水性碳酸钙粉体,化学成份要求CaCO3≥95.0%;纳米氧化铁系FeO和Fe2O3,为粒度小于100nm的粉体,化学成份要求其纯度≥90.0%;纳米二氧化硅为粒度小于100nm的粉体,化学成份要求其纯度≥98.5%。 The nano - calcium carbonate used refers to the hydrophilic calcium carbonate powder with a particle size of less than 100nm. Its purity is required to be ≥90.0%; nano-silica is a powder with a particle size of less than 100nm, and its chemical composition requires its purity to be ≥98.5%.
在本发明中,石灰的CaO含量要求≥96.0%,以水乳状形式加入,石灰乳的比重为1.2~1.3;萤石粉的纯度要求≥80.0%。In the present invention, the CaO content of the lime is required to be ≥ 96.0%, and it is added in the form of water emulsion, and the specific gravity of the lime milk is 1.2-1.3; the purity of the fluorite powder is required to be ≥ 80.0%.
本发明采用的结合剂亚硫酸纸浆废液(比重为1.1~1.2)为临时性结合剂,只为硅砖成型提供坯体的强度,高温下则通过液相烧结使其致密化并产生强度。The binder sulfurous acid pulp waste liquid (specific gravity 1.1-1.2) used in the present invention is a temporary binder, which only provides the strength of the green body for the molding of silica bricks, and densifies and generates strength through liquid phase sintering at high temperatures.
本发明的含有多种纳米粉硅砖的制备方法为:先预混合纳米粉以外的细粉部分,将纳米碳酸钙、纳米氧化铁和纳米二氧化硅在水中预分散制成浆体,在混碾机中将颗粒、混合粉、三种纳米粉的混合浆体、石灰乳、亚硫酸纸浆废液充分混合均匀后,用机器压制成砖坯,将坯体干燥至残余水分不大于1%后,在倒焰窑、梭式窑或隧道窑中烧成,最高烧成温度不大于1420℃,即制得本发明的纳米复合硅砖。The preparation method of the silica brick containing various nanometer powders of the present invention is as follows: first premix the fine powder part other than the nanometer powder, predisperse nanometer calcium carbonate, nanometer iron oxide and nanometer silicon dioxide in water to form a slurry, and mix In the mill, the granules, mixed powder, mixed slurry of three kinds of nano-powders, milk of lime, and sulfurous acid pulp waste liquid are fully mixed and uniform, and then pressed into bricks by machine, and dried until the residual moisture is not more than 1%. Firing in a downdraft kiln, a shuttle kiln or a tunnel kiln, the highest firing temperature is not higher than 1420°C to obtain the nanocomposite silica brick of the present invention.
本发明具有以下优点:The present invention has the following advantages:
1、由于纳米碳酸钙粒度小,在较低的温度(约690℃)下即开始分解,800℃时已基本分解完全。分解生成的纳米级氧化钙微粒具有很高的比表面积和反应活性,并在硅砖内部高度均匀分散。硅砖在烧成过程中,纳米级氧化钙与硅石反应产生高效矿化作用,从而达到促进烧结和提高性能的目的。1. Due to the small particle size of nano-calcium carbonate, it begins to decompose at a relatively low temperature (about 690°C), and it is basically completely decomposed at 800°C. The nano-scale calcium oxide particles generated by decomposition have high specific surface area and reactivity, and are highly uniformly dispersed inside the silica brick. During the firing process of silica bricks, nano-scale calcium oxide reacts with silica to produce high-efficiency mineralization, thereby achieving the purpose of promoting sintering and improving performance.
2、由于纳米氧化铁(FeO和Fe2O3)粒度细小,可以在硅砖内部高度均匀分散,在烧成过程中产生高效矿化作用,促进烧结,并使硅砖具有更均匀的组织结构,因而可以提高制品的强度和抗热震性能。2. Due to the fine particle size of nano-iron oxide (FeO and Fe 2 O 3 ), it can be highly uniformly dispersed inside the silica brick, which can produce high-efficiency mineralization during the firing process, promote sintering, and make the silica brick have a more uniform structure , which can improve the strength and thermal shock resistance of the product.
3、由于纳米二氧化硅粉体粒度细小,可以填充微细气孔,从而降低制品的气孔率,提高体积密度。3. Due to the fine particle size of nano-silica powder, it can fill fine pores, thereby reducing the porosity of the product and increasing the bulk density.
4、含复合纳米粉(纳米碳酸钙、纳米氧化铁、纳米二氧化硅)的硅砖生产工艺没有因使用纳米而改变,不需增加设备,保持了现有硅砖的生产工艺,适合大规模工业化生产。4. The production process of silica bricks containing composite nano-powder (nano-calcium carbonate, nano-iron oxide, nano-silicon dioxide) has not been changed due to the use of nano-powder, no need to increase equipment, and the existing production process of silica bricks is maintained, suitable for large-scale Industrial production.
5、本发明所用的纳米碳酸钙、纳米氧化铁、纳米二氧化硅不含有污染排放物,不含放射性,其加入形式为预分散成浆体,因此利用率高,无粉尘污染。5. The nano-calcium carbonate, nano-iron oxide, and nano-silicon dioxide used in the present invention do not contain polluting discharges, do not contain radioactivity, and are added in the form of pre-dispersion into a slurry, so the utilization rate is high and there is no dust pollution.
6、本发明所用的纳米碳酸钙、纳米氧化铁、纳米二氧化硅来源容易,相对其它氧化物纳米粉而言价格较低,适用于工业生产。6. The nano-calcium carbonate, nano-iron oxide, and nano-silicon dioxide used in the present invention are easy to source, relatively low in price compared with other oxide nanopowders, and suitable for industrial production.
具体实施方式Detailed ways
本发明的特点在于通过引入纳米碳酸钙、纳米氧化铁以及纳米二氧化硅,使硅砖在烧成过程中由于晶型转变而引起的体积膨胀得到抑制,促进了石英的转化,降低了气孔率,提高了体积密度、促进了烧结,提高了强度,改善了抗热震性。含复合纳米粉的硅砖其生产工艺与目前的生产工艺相同,主要原料(包括骨料和细粉)为硅石和废硅砖,二者配合使用。The feature of the present invention is that by introducing nano-calcium carbonate, nano-iron oxide and nano-silicon dioxide, the volume expansion of silica bricks caused by crystal transformation during the firing process is suppressed, the conversion of quartz is promoted, and the porosity is reduced. , Increased bulk density, promoted sintering, increased strength, and improved thermal shock resistance. The production process of silica bricks containing composite nano powder is the same as the current production process. The main raw materials (including aggregate and fine powder) are silica and waste silica bricks, and the two are used together.
下面举例说明本发明的实施及特点,但本发明不局限于下述实施例。为充分说明本发明的特点,对每一实施例给出了相应的实际生产技术的对比样,对比样通过加入氧化铁细粉(≤0.088mm)和石灰乳(引入氧化钙)作矿化剂,引入氧化铁和氧化钙的含量与实施例相当,二者进行对比。The following examples illustrate the implementation and characteristics of the present invention, but the present invention is not limited to the following examples. In order to fully illustrate the characteristics of the present invention, the comparative sample of the corresponding actual production technology is provided for each embodiment, and the comparative sample is made mineralizer by adding iron oxide fine powder (≤0.088mm) and milk of lime (introducing calcium oxide) , the content of introducing iron oxide and calcium oxide is equivalent to that of the examples, and the two are compared.
实施例1:各组份配比为(质量百分数)骨料(其中硅石颗粒52%,废硅砖颗粒8%,)60%,硅石粉35%,纳米碳酸钙粉体2.0%,纳米氧化铁0.5%,纳米二氧化硅1.5%,石灰0.5%,萤石粉0.5%,亚硫酸纸浆废液2%(外加)。Example 1: The proportioning of each component is (mass percentage) aggregate (wherein silica particles 52%, waste silica brick particles 8%) 60%, silica powder 35%, nano-calcium carbonate powder 2.0%, nano-iron oxide 0.5%, nano silicon dioxide 1.5%, lime 0.5%, fluorite powder 0.5%, sulfurous acid pulp waste liquid 2% (additional).
对比例1:各组份配比为(质量百分数)骨料(硅石和废硅砖颗粒)60%,硅石粉36.5%,氧化铁粉0.5%,石灰2.0%,萤石粉0.5%,亚硫酸纸浆废液2%(外加)。Comparative example 1: The proportion of each component is (mass percentage) aggregate (silica and waste silica brick particles) 60%, silica powder 36.5%, iron oxide powder 0.5%, lime 2.0%, fluorite powder 0.5%, sulfurous acid pulp Waste liquid 2% (additional).
实施例2:各组份配比为(质量百分数)骨料(其中硅石颗粒55%,废硅砖颗粒10%)65%,硅石粉28.5%,纳米碳酸钙粉体1.0%,纳米氧化铁1.0%,纳米二氧化硅2.0%,石灰1.5%,萤石粉1.0%,亚硫酸纸浆废液1.5%(外加)。Embodiment 2: The proportioning of each component is (mass percentage) aggregate (wherein silica particle 55%, waste silica brick particle 10%) 65%, silica powder 28.5%, nano-calcium carbonate powder 1.0%, nano-iron oxide 1.0 %, nano silicon dioxide 2.0%, lime 1.5%, fluorite powder 1.0%, sulfurous acid pulp waste liquid 1.5% (additional).
对比例2:各组份配比为(质量百分数)骨料(硅石和废硅砖颗粒)65%,硅石粉31.5%,氧化铁1.0%,石灰1.5%,萤石粉1.0%,亚硫酸纸浆废液1.5%(外加)。Comparative example 2: The ratio of each component is (mass percentage) aggregate (silica and waste silica brick particles) 65%, silica powder 31.5%, iron oxide 1.0%, lime 1.5%, fluorite powder 1.0%, sulfurous acid pulp waste Liquid 1.5% (additional).
实施例3:各组份配比为(质量百分数)骨料(其中硅石颗粒55%,废硅砖颗粒15%)70%,硅石粉24.5%,纳米碳酸钙粉体0.8%,纳米氧化铁1.5%,纳米二氧化硅1.2%,石灰1.0%,萤石粉0.5%,亚硫酸纸浆废液1.0%(外加)。Embodiment 3: the proportioning of each component is (mass percentage) aggregate (wherein silica particle 55%, waste silica brick particle 15%) 70%, silica powder 24.5%, nano-calcium carbonate powder 0.8%, nano-iron oxide 1.5% %, nano silicon dioxide 1.2%, lime 1.0%, fluorite powder 0.5%, sulfurous acid pulp waste liquid 1.0% (additional).
对比例3:各组份配比为(质量百分数)骨料(硅石和废硅砖颗粒)70%,硅石粉26.0%,氧化铁1.5%,石灰2.0%,萤石粉0.5%,亚硫酸纸浆废液1.0%(外加)。Comparative example 3: the proportion of each component is (mass percentage) aggregate (silica and waste silica brick particles) 70%, silica powder 26.0%, iron oxide 1.5%, lime 2.0%, fluorite powder 0.5%, sulfurous acid pulp waste Liquid 1.0% (additional).
按上述比例,将纳米粉以外的细粉部分先预混均匀,将纳米碳酸钙、纳米氧化铁和纳米二氧化硅在水中预分散制成浆体,在混碾机中将颗粒、混合粉、三种纳米粉的混合浆体、石灰乳、亚硫酸纸浆废液充分混合均匀后,用机器压制成砖坯,将坯体干燥至残余水分不大于1%后,在倒焰窑、梭式窑或隧道窑中烧成,最高烧成温度不大于1420℃,即制得本发明的含复合纳米硅砖,其性能见下附表。According to the above ratio, pre-mix the fine powder part other than the nano-powder evenly, pre-disperse the nano-calcium carbonate, nano-iron oxide and nano-silicon dioxide in water to make a slurry, and mix the particles, mixed powder, After the mixed slurry of three kinds of nanometer powder, lime milk, and sulfurous acid pulp waste liquid are fully mixed, they are pressed into bricks with a machine, and the bricks are dried until the residual moisture is not more than 1%. Firing in a tunnel kiln, the highest firing temperature is not higher than 1420°C, that is, the composite nano-silicon-containing brick of the present invention is obtained, and its properties are shown in the attached table.
附表:Schedule:
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